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US2767518A - Forehearth structure - Google Patents

Forehearth structure Download PDF

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Publication number
US2767518A
US2767518A US331055A US33105553A US2767518A US 2767518 A US2767518 A US 2767518A US 331055 A US331055 A US 331055A US 33105553 A US33105553 A US 33105553A US 2767518 A US2767518 A US 2767518A
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forehearth
glass
channel
burner
tubes
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US331055A
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Arthur W Schmid
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    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03BMANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B7/00Distributors for the molten glass; Means for taking-off charges of molten glass; Producing the gob, e.g. controlling the gob shape, weight or delivery tact
    • C03B7/02Forehearths, i.e. feeder channels
    • C03B7/06Means for thermal conditioning or controlling the temperature of the glass

Definitions

  • Claim. (Cl. 49-54) This invention relates to new and useful improvements in forehearth structures for use in conditioning molten glass for suspended charge, or the like, feeding, the forehearth being interposed between the glass melting tank and the feeder spout or bowl.
  • Fig. l is a side elevational view partially in cross section of a forehearth structure embodying the principles of this invention.
  • Fig. 2 is a vertical section taken along the line 22 of Fig. 1.
  • the numeral 1 designates a steel casing lined with insulating material 2 and 3 surrounding the forehearth refractory tile 4 which forms a trough 5 for retaining the glass as it is delivered from the glass melting tank that would be located on the right hand end of the forehearth as viewed in Fig. 1 to the feeder spout or boot designated by the numeral 6 rat the left hand end of the forehearth as viewed in Fig. l.
  • the forehearth is flanged as shown in 7, Fig. 2 to provide space for a side wall consisting of refractory tile 8 and insulating material 9 with a steel casing 19.
  • the roof is constructed of refractory tile 11 that extends over to form a part of the side wall.
  • the tiles 8 and 11 are provided with flue passages generally designated by the numeral 12 to form an L-shaped flue and the roof tile 11 is further provided with a conical shaped burner opening 13.
  • Disposed through openings 14 in the roof tile 11 are a plurality of refractory tubes 15 supported on the roof tile by a flange 16, the tube 15 extending downwardly through the treating chamber designated by the numeral 17 above the forehearth trough S in which the level of the glass is indicated by a line 18.
  • a series of tubes 15 are disposed longitudinally of the forehearth and they are provided with dampers 19 with an accessible lever 20 for regulating the opening.
  • the lines 12 may be regulated by blocks 21, Fig. 2, and peep holes 22 with covers 23 are provided as shown in Fig. 2.
  • Combustion air is supplied above the burner ports 13 by ducts 24 which constitute a manifold for all of the burners, and cooling air is supplied through a duct 25 common to all of the cooling tubes 15.
  • the fuel is supplied by a main 26 having manifolds 27 with burner nozzles 28 extending downwardly to the burner ports 13 in the manner shown in Fig. 2, each burner nozzle being provided with a valve 29 so that they may be-individually regulated.
  • a skimmer block 30 is provided to extend into the forehearth channel 5 to prevent the surface glass passing from the tank into the forehearth.
  • a partition 31 divides the forehearth into a heating zone on the right hand side of the partition 31 as viewed in Fig. 1, and a tempering or conditioning zone to the left of the partition block.
  • the feeder boot is provided with a feeding orifice 32 through which the glass is fed in suspended gobs that are sheared off and delivered to the forming molds.
  • the boot is provided with a refractory top 33 surrounded by a burner manifold 34, the top being provided with burner ports 35 as shown.
  • the conditioning zone is provided with the air manifold 24, the fuel manifold 27, the burner ports 13 and the burners 28, the same as the heating zone on the right hand side of the partition block 31.
  • the cooling system consisting of the tubes 15 and the air manifold 25 is eliminated in the tempering or conditioning zone.
  • the operation of the above described forehearth structure is briefly as follows.
  • the glass is fed from the tank and passes under the skimmer block 30 into the trough 5 where it is subjected to the heat of the series of burners which are of a special design that does not constitute a part of the present invention.
  • the burners function to extend the burner flame downwardly to the upper edge of the trough 5 to maintain the glass in channel 5 at a temperature that provides for constant circulation or movement of the glass along the edges of the channel to prevent devitrification. In doing this, however, the glass in the center of the channel may 'be heated excessively and for this reason a blast of cold air is supplied through the refractory tubes 15 to the center of the glass channel above the surface of the glass.
  • the cooling air from tubes 15 and the products of combustion from the burner 13 pass out of the treating chamber 17 through the flues 12, and by regulating the heat of the burners and the supply of cooling air together with the degree of opening of the flues 12 controlled by the damper blocks 21, a suitable heating condition can be maintained throughout the length of the forehearth.
  • a suitable heating condition can be maintained throughout the length of the forehearth.
  • the burner manifold 34 above the feeder boot further prevents cooling of the glass which is maintained preferably in a swirling motion to assure that the glass is of a uniform temperature and quality when it reaches the feeding orifice 32.
  • a glass flow channel extending longitudinally thereof having an enlarged treating chamber above the channel forming a shoulder at the top of the channel, fiues extending from the shoulder through the wall of the forehearth, burner ports in the roof of the forehearth structure for directing the flame vertically downward to the shoulder portion of the flow channel, and means for supplying a cooling medium centrally above the glass flow channel at the bottom of the treating chamber, said means comprising refractory tubes connected to a source of cooling air terminating substantially adjacent the glass level of the channel.

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  • Chemical & Material Sciences (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Furnace Details (AREA)

Description

Oct. 23, 195% A. w. SCHMID 2,767,518
.FOREHEARTH STRUCTURE Fi led Jan. 15, 1953 2 Sheets-Sheet 1 INVENTOR. Ma 135M Oct. 23, 1956 w. SCHMID 2,767,513
FOREHEARTH STRUCTURE.
Filed Jan. 13, 1953' 2 Sheets-sheaf, 2
INVENTOR. M m BY 2% 05M United States Patent FOREHEARTH STRUCTURE Arthur W. Schmid, Pittsburgh, Pa. Application January 13, 1953, Serial No. 331,055
1 Claim. (Cl. 49-54) This invention relates to new and useful improvements in forehearth structures for use in conditioning molten glass for suspended charge, or the like, feeding, the forehearth being interposed between the glass melting tank and the feeder spout or bowl.
Some of the difficulties encountered in the feeding of glass is the maintenance of suitable temperatures and the prevention of stagnation which results when some of the glass accumulates along the walls of the forehearth due to improper circulation and temperature controls.
It is among the objects of the present invention to provide for the proper heating of the glass throughout the forehearth while maintaining proper temperatures for feeding through the application of a cooling medium.
The invention will become more apparent from a consideration of the accompanying drawings constituting a part hereof in which like reference characters designate like parts and in which:
Fig. l is a side elevational view partially in cross section of a forehearth structure embodying the principles of this invention, and
Fig. 2 is a vertical section taken along the line 22 of Fig. 1.
With reference to the several figures of the drawing the numeral 1 designates a steel casing lined with insulating material 2 and 3 surrounding the forehearth refractory tile 4 which forms a trough 5 for retaining the glass as it is delivered from the glass melting tank that would be located on the right hand end of the forehearth as viewed in Fig. 1 to the feeder spout or boot designated by the numeral 6 rat the left hand end of the forehearth as viewed in Fig. l. The forehearth is flanged as shown in 7, Fig. 2 to provide space for a side wall consisting of refractory tile 8 and insulating material 9 with a steel casing 19.
The roof is constructed of refractory tile 11 that extends over to form a part of the side wall. The tiles 8 and 11 are provided with flue passages generally designated by the numeral 12 to form an L-shaped flue and the roof tile 11 is further provided with a conical shaped burner opening 13. Disposed through openings 14 in the roof tile 11 are a plurality of refractory tubes 15 supported on the roof tile by a flange 16, the tube 15 extending downwardly through the treating chamber designated by the numeral 17 above the forehearth trough S in which the level of the glass is indicated by a line 18. As shown in Fig. 1, a series of tubes 15 are disposed longitudinally of the forehearth and they are provided with dampers 19 with an accessible lever 20 for regulating the opening. Also the lines 12 may be regulated by blocks 21, Fig. 2, and peep holes 22 with covers 23 are provided as shown in Fig. 2.
Combustion air is supplied above the burner ports 13 by ducts 24 which constitute a manifold for all of the burners, and cooling air is supplied through a duct 25 common to all of the cooling tubes 15. The fuel is supplied by a main 26 having manifolds 27 with burner nozzles 28 extending downwardly to the burner ports 13 in the manner shown in Fig. 2, each burner nozzle being provided with a valve 29 so that they may be-individually regulated.
With reference to Fig. 1 of the drawing, a skimmer block 30 is provided to extend into the forehearth channel 5 to prevent the surface glass passing from the tank into the forehearth. A partition 31 divides the forehearth into a heating zone on the right hand side of the partition 31 as viewed in Fig. 1, and a tempering or conditioning zone to the left of the partition block. The feeder boot is provided with a feeding orifice 32 through which the glass is fed in suspended gobs that are sheared off and delivered to the forming molds. The boot is provided with a refractory top 33 surrounded by a burner manifold 34, the top being provided with burner ports 35 as shown. The conditioning zone is provided with the air manifold 24, the fuel manifold 27, the burner ports 13 and the burners 28, the same as the heating zone on the right hand side of the partition block 31. The cooling system consisting of the tubes 15 and the air manifold 25 is eliminated in the tempering or conditioning zone.
The operation of the above described forehearth structure is briefly as follows. The glass is fed from the tank and passes under the skimmer block 30 into the trough 5 where it is subjected to the heat of the series of burners which are of a special design that does not constitute a part of the present invention. The burners function to extend the burner flame downwardly to the upper edge of the trough 5 to maintain the glass in channel 5 at a temperature that provides for constant circulation or movement of the glass along the edges of the channel to prevent devitrification. In doing this, however, the glass in the center of the channel may 'be heated excessively and for this reason a blast of cold air is supplied through the refractory tubes 15 to the center of the glass channel above the surface of the glass.
The cooling air from tubes 15 and the products of combustion from the burner 13 pass out of the treating chamber 17 through the flues 12, and by regulating the heat of the burners and the supply of cooling air together with the degree of opening of the flues 12 controlled by the damper blocks 21, a suitable heating condition can be maintained throughout the length of the forehearth. As the glass is being fed from the orifice 32, it exerts a constant pull through the forehearth channel 5 and when the glass is delivered to the conditioning zone on the left side of the partition block 31, its temperature conditions are properly maintained by the series of burners in that zone. The burner manifold 34 above the feeder boot further prevents cooling of the glass which is maintained preferably in a swirling motion to assure that the glass is of a uniform temperature and quality when it reaches the feeding orifice 32.
It is evident from the foregoing description of this invention that forehearth structures embodying the firing and cooling principles herein described and shown, provide for positive regulation of temperature and conditioning of the glass.
Although one embodiment of the invention has been herein illustrated and described, it will be evident to those skilled in the art that various modifications may be made in the details of construction without departing from the principles herein set forth.
I claim:
In a forehearth for conditioning glass, a glass flow channel extending longitudinally thereof having an enlarged treating chamber above the channel forming a shoulder at the top of the channel, fiues extending from the shoulder through the wall of the forehearth, burner ports in the roof of the forehearth structure for directing the flame vertically downward to the shoulder portion of the flow channel, and means for supplying a cooling medium centrally above the glass flow channel at the bottom of the treating chamber, said means comprising refractory tubes connected to a source of cooling air terminating substantially adjacent the glass level of the channel.
References Cited in the file of this patent UNITED STATES PATENTS 1,893,061 Peiler Jan. 3, 1933 4- Honiss Aug. 14, 1934 Wardley Aug. 14, 1934 Peiler Dec. 13, 1938 Honiss Jan. 24, 1939 Koob DBC.24, 1940 Ferngren Oct. 20, 1942 Grifiin Nov. 2, 1952 Hess M Nov. 25, 1952
US331055A 1953-01-13 1953-01-13 Forehearth structure Expired - Lifetime US2767518A (en)

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Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3353941A (en) * 1964-05-29 1967-11-21 Emhart Corp Method of melting glass
DE1278319B (en) * 1963-11-28 1969-04-17 Bbc Brown Boveri & Cie Process for protecting surface parts of a heat-resistant body that have been swept over by hot media
DE1596575B1 (en) * 1967-04-24 1971-07-15 Owens Corning Fiberglass Corp METHOD AND DEVICE FOR REGULATING THE TEMPERATURE OF MELTED GLASS
DE2410763A1 (en) * 1973-03-06 1974-09-19 Emballage Ste Gle Pour FEEDER FOR MELTED GLASS
US4069032A (en) * 1976-05-04 1978-01-17 Societe Generale Pour L'emballage Forehearth for glass furnace
DE3412639A1 (en) * 1984-04-04 1985-10-24 Himly, Holscher GmbH & Co, 3070 Nienburg Process for equalising the temperature over the cross-section of a stream of glass and forehearth for carrying out the process
EP0223866A1 (en) * 1985-09-24 1987-06-03 Himly, Holscher GmbH & Co. Method for equilibrating the temperature in the transversal sense of a glass stream, and feeder channel used therefor
US4750928A (en) * 1987-06-25 1988-06-14 Glass Technology Development Corporation Conduit for molten glass
EP0403289A1 (en) * 1989-06-16 1990-12-19 Ardagh Glass Limited Method and apparatus for equalization of temperature in a forehearth in glass manufacture
EP0484162A3 (en) * 1990-10-31 1993-01-13 Clive Ward Method and apparatus for conveying molten glass

Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1893061A (en) * 1929-09-19 1933-01-03 Hartford Empire Co Forehearth for molten glass
US1970113A (en) * 1928-05-08 1934-08-14 Hartford Empire Co Forehearth for glass melting furnaces and method of conditioning molten glass
US1970094A (en) * 1930-01-25 1934-08-14 Hartford Empire Co Means for and method of controlling the temperature and condition of molten glass in forehearths
US2139770A (en) * 1935-09-24 1938-12-13 Hartford Empire Co Forehearth for molten glass
US2144973A (en) * 1937-04-01 1939-01-24 Hartford Empire Co Forehearth for molten glass
US2226498A (en) * 1938-08-27 1940-12-24 Hartford Empire Co Glass melting and delivering apparatus and method
US2299084A (en) * 1937-11-27 1942-10-20 Enoch T Ferngren Sealing and insulating glass furnaces
US2616380A (en) * 1950-06-14 1952-11-04 Emhart Mfg Co Forehearth roof structure
US2618906A (en) * 1945-09-14 1952-11-25 Selas Corp Of America Glass melting furnace

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1970113A (en) * 1928-05-08 1934-08-14 Hartford Empire Co Forehearth for glass melting furnaces and method of conditioning molten glass
US1893061A (en) * 1929-09-19 1933-01-03 Hartford Empire Co Forehearth for molten glass
US1970094A (en) * 1930-01-25 1934-08-14 Hartford Empire Co Means for and method of controlling the temperature and condition of molten glass in forehearths
US2139770A (en) * 1935-09-24 1938-12-13 Hartford Empire Co Forehearth for molten glass
US2144973A (en) * 1937-04-01 1939-01-24 Hartford Empire Co Forehearth for molten glass
US2299084A (en) * 1937-11-27 1942-10-20 Enoch T Ferngren Sealing and insulating glass furnaces
US2226498A (en) * 1938-08-27 1940-12-24 Hartford Empire Co Glass melting and delivering apparatus and method
US2618906A (en) * 1945-09-14 1952-11-25 Selas Corp Of America Glass melting furnace
US2616380A (en) * 1950-06-14 1952-11-04 Emhart Mfg Co Forehearth roof structure

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1278319B (en) * 1963-11-28 1969-04-17 Bbc Brown Boveri & Cie Process for protecting surface parts of a heat-resistant body that have been swept over by hot media
US3353941A (en) * 1964-05-29 1967-11-21 Emhart Corp Method of melting glass
DE1596575B1 (en) * 1967-04-24 1971-07-15 Owens Corning Fiberglass Corp METHOD AND DEVICE FOR REGULATING THE TEMPERATURE OF MELTED GLASS
DE2410763A1 (en) * 1973-03-06 1974-09-19 Emballage Ste Gle Pour FEEDER FOR MELTED GLASS
US4069032A (en) * 1976-05-04 1978-01-17 Societe Generale Pour L'emballage Forehearth for glass furnace
DE3412639A1 (en) * 1984-04-04 1985-10-24 Himly, Holscher GmbH & Co, 3070 Nienburg Process for equalising the temperature over the cross-section of a stream of glass and forehearth for carrying out the process
EP0223866A1 (en) * 1985-09-24 1987-06-03 Himly, Holscher GmbH & Co. Method for equilibrating the temperature in the transversal sense of a glass stream, and feeder channel used therefor
US4750928A (en) * 1987-06-25 1988-06-14 Glass Technology Development Corporation Conduit for molten glass
EP0403289A1 (en) * 1989-06-16 1990-12-19 Ardagh Glass Limited Method and apparatus for equalization of temperature in a forehearth in glass manufacture
US5055123A (en) * 1989-06-16 1991-10-08 Ardagh Glass Limited Method and apparatus for equalization of temperature in a forehearth in glass manufacture
AU624774B2 (en) * 1989-06-16 1992-06-18 Zedtec Limited Method and apparatus for equalization of temperature in a forehearth in glass manufacture
EP0484162A3 (en) * 1990-10-31 1993-01-13 Clive Ward Method and apparatus for conveying molten glass

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